Nickel Catalyst Ethylene Dimerization Butene-1 Selectivity

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Solution Overview

Problem

Existing processes for dimerizing ethylene into butene-1 suffer from inefficiencies in yield and selectivity, with previous methods often resulting in lower production rates and mixed product distributions.

Innovation Solution

A catalytic composition comprising a nickel precursor with an oxidation state of +II, at least one phosphine ligand, and an activating agent, such as chlorinated or brominated hydrocarbylaluminum compounds, operating within a temperature range of 45°C to 250°C, with specific molar ratios of phosphine to nickel and activating agent to phosphine, enhances the selective production of butene-1.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If existing nickel-based catalytic systems with phosphine ligands are used for ethylene dimerization, then the process can proceed, but the yield and selectivity for butene-1 production are insufficient

Engineering Contradiction:
Improvebutene-1 production efficiencyVSAvoidbutene-1 selectivity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent changes the oxidation state parameter of the nickel catalyst from 0 to +2, and optimizes the phosphine-to-nickel molar ratio parameter to between 0.5 and 5. These parameter changes result in improved butene-1 selectivity (at least 62%) and yield (at least 91%), resolving the contradiction between productivity and manufacturing precision.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If previous dimerization processes are used, then butenes can be produced, but the product distribution is mixed and the production rate is low

Engineering Contradiction:
Improveproduction rateVSAvoidproduct distribution uniformity
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The patent optimizes key parameters including raising the nickel oxidation state to +2, adjusting the phosphine-to-nickel molar ratio to 0.5-5, and setting the reaction temperature between 20-250°C. These parameter changes achieve a production rate of at least 91% butene yield with stable product distribution (at least 62% butene-1 selectivity), resolving the contradiction between productivity and composition stability.

Inventive Principle:
Principle #35Parameter changes

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The process achieves a butene (C4) yield of at least 91% and a butene-1 selectivity of at least 62%, significantly improving the efficiency and selectivity of butene-1 production compared to previous methods.

Implementation Method 1

The transformation of ethylene using a homogeneous nickel catalyst has been studied since 1950. This research has led to the development and commercialization of different processes.

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentEP3328542B1Ethylene dimerization process
Publication Date: 2021.09.08 IFP ENERGIES NOUVELLES

AI summary

The invention relates to a method for the dimerisation of ethylene into butene-1 carried out with a catalytic composition comprising: at least one nickel precursor with a degree of oxidation (+II); at least one phosphine ligand of formula PR1R2R3, in which groups R1,R2 and R3 may be identical or different and may or may not be bonded to one another; and at least one activating agent selected from the group containing the chlorinated or brominated compounds of hydrocarbylaluminium, either alone or in admixture, said composition having a molar ratio of phosphine ligand to nickel precursor of between 5 and 30 and a molar ratio of activating agent to phosphine ligand greater than or equal to 1.